Polymeric complex supporter with zero-valent metals and manufacturing method thereof

ABSTRACT

A zero-valent metal polymeric complex supporter (ZVM-PCS) is disclosed. The PCS possesses porous surface and internal coralloid-like channel structure that can accommodate high amount of iron-containing materials and derivatives thereof. The surface pore size, porosity, hydrophilicitv, and internal coralloid-like channel structure of PCS can be tailored through the manufacturing process, with which PCS can be functioned as a regulator for the releasing of produced hydrogen, and also control the adsorption and reactions toward heavy metals and chlorinated volatile organic compounds in water. The hydrogen released from the ZVM-PCS can be applied to anaerobic bioremediation. Moreover, the ZVM-PCS can be filter materials that can be installed in a column or any storage for water and wastewater treatment, or even in a groundwater cut-off barrier for the cleanup of contamination. While the ZVM-PCS is synthesized as a film without surface openings, it can be used as the electromagnetic interference (EMI) shielding material.

RELATED APPLICATIONS

The present application is based on, and claims priority from, TaiwanApplication Ser. No. 100132459, filed Sep. 8. 2011, the disclosure ofwhich is hereby incorporated by reference herein in its entirety.

FIELD OF THE INVENTION

This invention generally relates to a polymeric complex supporter (PCS)with zero-valent metals and a method for manufacturing the same; andmore particularly, to a PCS comprising iron-containing materials andderivatives thereof and a method for manufacturing the same, which canbe applied on pollution remediation and electromagnetic interferenceshielding.

BACKGROUND OF THE INVENTION

It has been proved by many related researches since 1990s that micro ornano scale zero-valent iron (ZVI) is a very effective material for soiland groundwater remediation. Contaminants such as chlorinated volatileorganic compounds, heavy metals, pesticides, PCBs and dioxins can bedegraded by ZVI. Nano-scale ZVI can react faster due to smaller particlesize and larger surface area. However, the bare nanoscale ZVI is alsoeasy to be corroded, which thus shortens its longevity. Currently, ZVI'sapplications are still restricted in the groundwater environment whereis a hypoxic or anoxic condition. It is barely seen that ZVI is appliedto water or wastewater treatment system that might be due to the highercost, higher water chroma and turbidity, difficult recycling andseparation, and so on. On the other hand, ZVI has the characteristics ofhydrogen production and magnetism, which is not yet fully developed.

Zero-valent metals (ZVMs), for example, ZVI (Fe⁰), zero-valent zinc(Zn⁰) and zero-valent aluminum (Al⁰), have excellent reduction abilityto decompose water and generate hydrogen. For the commonly-used slurrytype of ZVM, the generated hydrogen is usually mixed with ZVM powders inthe slurry and thus is hard to be used more efficiently. Moreover, ZVMpowders relatively have more surface areas exposed to air, that mayshorten the longevity and increase the cost.

It has been shown that the ZVM powders can be coated with organicsubstances (for example, polymers and surfactants) or inorganicsubstances (for example, silicon dioxide and titanium dioxide) to slowdown the corrosion rate and to increase reaction rate. However, thatstill cannot extend the ZVM materials into various application fields.

Therefore, it should be necessary to provide a better method formanufacturing zero-valent metals, which strengthens the originalfeatures and produces more industrial applications of ZVMs.

SUMMARY OF THE INVENTION

Accordingly, an aspect of the present invention provides a zerovalentmetal-polymer complex supporter (ZVM-PCS) that can accommodate highamount (up to approximately 92 parts by weight) of iron-containingmaterials and derivatives thereof and control the hydrogen-releasingrate. The surface pore size, porosity, hydrophilicity, and internalcoralloid-like channel structure of PCS can be tailored through themanufacturing process, so that PCS can be functioned as a regulator forthe release of produced hydrogen, and also control the adsorption andreactions toward heavy metals and chlorinated volatile organic compoundsin water. The released hydrogen from the ZVM-PCS thus provides therequired gas for metabolism of anaerobic microbes. Moreover, the ZVM-PCScan be applied to filter materials of water and wastewater treatment andcut-off walls of groundwater pollution remediation, thereby adsorbingheavy metals and catalyzing reduction reactions of chlorinated volatileorganic compounds.

Another aspect of the present invention provides a method formanufacturing ZVM-PCS, which is combined with both wet- and dry-formingand functionalizing step of the PCS. Iron-containing materials andderivatives thereof are embedded into a three-dimensional internal spacein the PCS. The surface pore size, porosity, hydrophilicity, andinternal coralloid-like channel structure of the PCS can be tailored,with which PCS can be functioned as a regulator for controlling thehydrogen-released rate of the iron-containing materials and derivativesthereof.

A still another aspect of the present invention provides a method formanufacturing ZVM-PCS, which includes a dry-forming and functionalizingstep for iron-containing materials and derivatives thereof to beembedded into a three-dimensional internal space in PCS, so as to form aZVM-PCS which is flexible and has a dense structure without surfaceopenings.

A further aspect of the present invention provides a ZVM-PCS that ismanufactured by the above-described method. The ZVM-PCS is flexible andhas a dense nonporous structure that can be used as the electromagneticinterference (EMI) shielding material.

According to the aforementioned aspect of the present invention, ZVM-PCSis disclosed. In an embodiment, PCS may include but not limited to 1part to 92 parts by weight of iron-containing materials and derivativesthereof and 8 parts to 99 parts by weight of polymers. As the ZVM-PCS isimmersed in a water-containing environment, water molecules diffuse intothe internal coralloid-like channel structure through surface pores andthen react with the iron-containing materials and derivatives thereof.The generated hydrogen can be continuously released out through surfacepores to promote microbial growth, and adsorption and/or degradation ofpollutants in water.

In a preferred embodiment, the aforementioned iron-containing materialsand derivatives thereof may include zero-valent irons (Fe⁰) that mayhave an averaged diameter from 1 nanometer (nm) to 10 micrometers (μm).

In a preferred embodiment, the aforementioned ZVM-PCS may possess aninternal coralloid-like channel structure and surface pores disposedthereon. The surface pores may have an averaged pore size from 1 nm to100 μm, for example.

In a preferred embodiment, the polymeric complexes may be sulfonepolymers or fluorine-containing polymers.

In a preferred embodiment, the aforementioned ZVM-PCS may furtherinclude an absorbing material, a heat dispersing, material, and/or abionutrient except for iron-containing materials and derivativesthereof.

In a preferred embodiment, the water-containing environment may refer toocean, river, lake, sewerage, ditch, aquifer, cistern, sludge or soil.

According to the another aspect of the present invention, a method formanufacturing ZVM-PCS is disclosed. In an embodiment, the method caninclude the following steps. First, a mixture is prepared, which caninclude but not limited to 1 part to 92 parts by weight ofiron-containing materials and derivatives thereof, 8 parts to 99 partsby weight of polymers, and an organic solvent. Next, vacuuming may beperformed to remove air bubbles in the mixture. Afterward, the mixtureis subjected to a forming and functionalizing step that may include butbe not limited to a wet-forming and functionalizing step and adry-forming and functionalizing step, so as to form the ZVM-PCS thataccommodates the iron-containing materials and derivatives thereof. Theresulted ZVM-PCS has an internal coralloid-like channel structure with aporous surface with tunable pore sizes from 1 nm to 100 μm. As theZVM-PCS is immersed in a water-containing environment, water moleculesdiffuse into the internal coralloid-like channel structure through thesurface pores and then react with iron-containing materials andderivatives thereof. The produced hydrogen may be continuously releasedout through the surface pores of PCS, and promote microbial growth andadsorption and/or degradation of pollutants in water. In a preferredembodiment, the ZVM-PCS may be shaped as various types, such as plate(e.g. flake or thin film), granule, hollow tube, rod or other solidtypes, depending on the demand of applications.

In a preferred embodiment, the method for manufacturing ZVM-PCS may beperformed in a batch process or an automatically continuous process.

According to the still another aspect of the present invention, a methodfor manufacturing ZVM-PCS is disclosed. In an embodiment, the method caninclude the following steps. Firstly, a mixture is prepared, which caninclude but be not limited to 1 part to 92 parts by weight ofiron-containing materials and derivatives thereof, 8 parts to 99 partsby weight of polymers, and an organic solvent, so as to dissolvepolymers and evenly disperse the iron-containing materials andderivatives thereof. Next, vacuuming may be performed to remove airbubbles in the mixture. Afterward, a dry forming and functionalizingstep may be performed to form the ZVM-PCS. The resulted ZVM-PCS thataccommodates the iron-containing materials and derivatives thereof isflexible and has a dense non-porous structure.

According to the further aspect of the present invention, anelectromagnetic interference (EMI) shielding material is provided, whichis synthesized by the aforementioned method. The EMI shielding materialis flexible and has a dense non-porous structure for effectivelyshielding electromagnetic waves.

In application of the aforementioned ZVM-PCS and manufacturing methodthereof, the ZVM-PCS has tunable surface pore sizes, porosity, affinitytoward water and the internal coralloid-like channel structure, so as toaccommodate high amount of iron-containing materials and derivativesthereof. The PCS can be functioned as a regulator for thehydrogen-releasing rate of the reaction with the ZVM-PCS and water, andalso control the adsorption rate and reduction rate toward heavy metalsand chlorinated volatile organic compounds in water. Therefore, thereleased hydrogen from the ZVM-PCS provides the requirement formetabolism of anaerobic microbes. Also, the ZVM-PCS can be applied towastewater filtration materials and cut-off walls of groundwaterpollution remediation for adsorption of heavy metals and catalysis ofreduction reactions of chlorinated volatile organic compounds.Furthermore, while the ZVM-PCS is formed to a poreless film as the EMIshielding material.

BRIEF DESCRIPTION OF THE DRAWINGS

The foregoing aspects and many of the attendant advantages of thisinvention are more readily appreciated as the same become betterunderstood by reference to the following detailed description inconjunction with the accompanying drawing, wherein:

FIG. 1 depicts a partial flow chart of a method for manufacturing theZVM-PCS according to an embodiment of the present invention.

FIG. 2 shows a hollow tube-like shape of the ZVI-PCS according to anembodiment of the present invention.

FIGS. 3A to 3C show the photographs of cross-sectional (FIG. 3A)internal (FIG. 3B) and superficial structures (FIG. 3C) of the ZVI-PCSaccording to several embodiments of the present invention.

FIG. 4 depicts an application diagram of replaceable columns accordingto an embodiment of the present invention.

FIG. 5 depicts a diagram of a permeable reactive barrier according toanother embodiment of the present invention.

FIG. 6 depicts a schematic diagram of a setup for measuring releasedhydrogen from the ZVI-PCS of EXAMPLE 1. FIG. 7 depicts a curve diagramof released hydrogen amount of the ZVI-PCS immersed in the device ofFIG. 6.

FIG. 8 depicts a curve diagram of oxidation-reduction potential of theZVI-PCS.

FIG. 9 depicts a curve diagram of molybdenum concentration of wastewatertreated with the ZVI-PCS.

FIGS. 10A to 10C show scanning electron microscopy image (FIG. 10A),energy dispersive spectrometry spectrum (FIG. 10B) and element linescanning (FIG. 10C) of the ZVI-PCS after treating wastewater.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

Accordingly, the present invention provides a polymeric complexsupporter (PCS) with zero-valent metals (ZVI-PCS) and a manufacturingmethod thereof, in which the PCS can accommodate high amount ofiron-containing materials and derivatives thereof in its internalcoralloid-like channel structure, so as to form the ZVI-PCS.

The “ZVI-PCS” described in the present invention refers to the PCS thataccommodates iron-containing materials and derivatives thereof. Thesurface pore size, porosity, the internal coralloid-like channelstructure and affinity toward water of the PCS can be tunable, therebycontinuously and stably releasing hydrogen gas generated from thereaction of iron-containing materials and derivatives thereof with waterfor a long period. Therefore, ZVI-PCS can be used to facilitate thegrowth of anaerobes, and the iron-containing materials and theirderivatives can absorb and degrade pollutants. In an embodiment, theZVI-PCS can accommodate high amount of hydrogen-releasing materials andderivatives thereof in the spacious structure.

“The internal coralloid-like channel structure” described in the presentinvention refers to the structure in PCS. The internal coralloid-likechannel structure is constructed by polymeric connections, where thediffusion of water and hydrogen molecules is constrained so that theproduced hydrogen can be continuously released for a long time.

“The iron-containing materials and derivatives thereof” described in thepresent invention refers to the substance that can release hydrogenafter contacting and reacting with water, also called hydrogen-releasingsubstance or hydrogen-generating substance. The iron-containingmaterials and derivatives thereof can contribute to the growth ofanaerobes, absorb and/or degrade pollutants. Also, thehydrogen-releasing rate of iron-containing materials and derivativesthereof depends on their particle size, for example, having 1 nm to 100μm of the averaged diameter.

In an embodiment, iron-containing materials and derivatives thereof mayinclude zero-valent iron (ZVI, Fe⁰) particles. In an example, the ZVImay be commercially available product that is either purified orcontains impurities. As the ZVI contacts and reacts with water, hydrogengas is then generated according to the following reaction formula (I),so as to facilitate growth of anaerobes, to absorb and/or to degradepollutants. Therefore, the ZVI-PCS also provides many functions asaforementioned.

Fe⁰+2H₂O→Fe²⁺+H₂+2OH⁻  (I)

As the above description, the PCS can accommodate high amount ofiron-containing materials and derivatives thereof. As the ZVI-PCS isimmersed in a water-containing environment, the higher high specificsurface area of the ZVI-PCS provides for quick diffusion of watermolecules and pollutants into the surface pores and the internalcoralloid-like channel structure, for being absorbed and degraded by theiron-containing materials and derivatives thereof. The carrier'sstructure can control and constrain the generation of the hydrogen gas,so that the hydrogen gas can be continuously released out and beneficialto anaerobic bioremediation.

“The water-containing environment” refers to all water-containingenvironments, which may include but be not limited to ocean, river,lake, sewerage, ditch, aquifer, cistern, sludge, soil or the likes.According to an embodiment, the ZVI-PCS provides some tunableproperties, such as the usage and averaged particle size of theiron-containing materials and derivatives thereof, the surface poresize, porosity, internal coralloid-like channel structure and affinitytoward water of the PCS, for strengthening the absorption and reactionof ZVI-PCS to pollutants as Well as continuously releasing gas for along period.

In addition, in order to enhance the catalytic or magnetic effect ofZVIs, noble metals can be attached onto the ZVIs. In an example, thenoble metals may be platinum, palladium, rhodium, gold, silver, cobaltor any combination thereof.

The iron-containing materials and derivatives thereof can absorb and/ordegrade “pollutants”. The “pollutants” described in the presentinvention refers to heavy metal pollutants, organohalogen compounds ornitrates. In an embodiment, the heavy metal pollutants may include butbe not limited to arsenic, molybdenum or chromium. The organohalogencompounds may include but be not limited to chlorinated volatile organiccompounds (CVOCs), trichloroethylene (TCE), perchloroethyler (PCE) ordioxins.

In an embodiment, the ZVI-PCS can accommodate more amounts ofiron-containing materials and its derivatives. In an example, theZVI-PCS may be formed by mixing 8 parts to 99 parts by weight ofpolymers and 1 part to 92 parts by weight of iron-containing materialsand derivatives thereof. In another example, the ZVI-PCS may be formedby mixing 8 parts to 95 parts by weight of polymers and 5 parts to 92parts by weight of iron-containing materials and derivatives thereof. Ina further example, ZVI-PCS may be formed by mixing 8 parts to 50 partsby weight of polymers and 50 parts to 92 parts by weight ofiron-containing materials and derivatives thereof.

In another embodiment, iron-containing materials and derivatives thereofmay have an averaged pore size from 1 nm to 10 μm. The PCS may have aninternal coralloid-like channel structure and a plurality of surfacepores with an averaged pore size from 1 nm to 100 μm for accommodatingmore amounts (for example, up to 92 parts by weight) of iron-containingmaterials and derivatives thereof. Moreover, depending on actualrequirements, the PCS can be made by using hydrophilic polymericmaterials, hdrophobic polymeric materials or any combination thereof, soas to control the PCS's affinity toward water. In an example, theaforementioned polymeric materials may be sulfone polymers orfluorine-containing polymers. The sulfone polymers may include but benot limited to polyethersulfone (PESF), polysulfone (PSF) orpolyphenylene sulfone (PPSF). The fluorine-containing polymers mayinclude polyvinylidene fluoride (PVDF).

In a further embodiment, the ZVI-PCS may optionally include otherabsorbent materials, heat dispersing materials and/or bionutrients forincreasing more functions. The usage of the absorbent materials, heatdispersing materials and/or bionutrients in ZVI-PCS is 0.01 part to 35parts by weight respectively based on the total weight of theiron-containing materials and derivatives thereof and the PCS. In anexample, the absorbent materials may include but be not limited toactivated carbon, zeolite, molecular sieve or any combination thereof.In another example, the heat dispersing materials may include but be notlimited to boron nitride, carbon nanotubes or any combination thereof.In a further example, the bionutrients may include but be not limited tosugar, starch or any combination thereof. The additions may also enhancethe growth of microorganisms in the water-containing environment.

In a further embodiment, the ZVI-PCS can be synthesized as a filmwithout surface openings, which accommodate high amount ofiron-containing materials and derivatives thereof. Therefore, it can beused as an EMI shielding material. In one example, the film may beoptionally added the heat dispersing materials for increasing morefunctions.

In a still another embodiment, ZVI-PCS may be manufactured as follows.Reference is made to FIG. 1, which depicts a partial flow chart of amethod for manufacturing ZVI-PCS according to an embodiment of thepresent invention. In an example, a mixture is firstly prepared, forexample, including 1 part to 92 parts by weight of the iron-containingmaterials and derivatives thereof, 8 parts to 99 parts by weight of thepolymers and an organic solvent as shown in the step 101. The polymerscan be dissolved and the iron-containing materials and derivativesthereof can be dispersed in the organic solvent. In this example, thepolymers may be exemplified as the aforementioned materials. The organicsolvent may include but be not limited to N,N-dimethyl formamide (DMF),1-methyl 2 pyrrolidione (NMP) and N,N-dimethylacetamide (DMAc). Inanother example, the iron-containing materials and derivatives thereofand polymers may be different contents of parts by weight beyondaforementioned in the mixture without being recited in detail herein. Ina further example, the mixture may optionally include absorbentmaterials, heat dispersing materials and/or bionutrients asaforementioned.

Following, a dispersion and stabilization step may be optionallyperformed as shown in the step 103, in which the dispersant may be addedand mixed at a stirring speed from 50 revolutions per minute (rpm) to500 rpm for 6 hours and 24 hours approximately until the mixture isevenly and stably dispersed without immediate sedimentation. Thus, theiron-containing materials are evenly dispersed in the resulted ZVI-PCS,and the PCS has smooth surface and uniform color. In an example, thedispersants may include organic polymeric dispersants such aspolycarboxylate, polyvinyl alcohol, polyacrylamide or any combinationthereof. In another example, an amount of the dispersant may be 0.1parts to 2 parts by weight based on the total weight of theiron-containing materials and derivatives thereof and the PCS. It shouldbe noted that, the organic polymeric dispersant may further includeother dispersants having the same or similar ingredients therein, suchas commercially availible dispersants of Hypermer™ KD-1, KD-2, KD-3,KD-4, KD-6, KD-7 and KD-9 manufactured by Croda InternationalPlc.England without being limited to the above examples. Next, avacuuming step may be carried out to remove air bubbles in the mixture.

Afterward, a formation and functionalizing step may be performed asshown in the step 105, in which the forming and functionalizing step mayinclude but be not limited to a wet-forming and functionalizing step (asshown in the step 105 a) and a dry-forming and functionalizing step (asshown in the step 105 b), so as to make the mixture to form the ZVI-PCSthat the iron-containing materials and derivatives thereof arecompletely received in the PCS.

In detail, in an embodiment, during performing the wet-forming andfunctionalizing step (as shown in the step 105 a), the mixture may beswollen in a coagulant under a temperature of 0° C. to 40° C. for 0.5minute to 5 minutes, for example, so as to partially remove the organicsolvent and the coagulant and to form a composite material. In anexample, the wet-forming and functionalizing step may be performed undera temperature of 5° C. to 15° C. In another example, an appropriatecoagulant solvent may include but be not limited to methanol, ethanol,propanol, acetone, water or any combination thereof. In this embodiment,for the purpose of formation of the composite materials with variousshapes, many conventional methods can be applied to form the compositematerial having various shapes such as plates (or flakes or films),granules, hollow tubes or bars. Those methods and shapes are well knownto the artisan in this art rather than being recited in detail herein.

In another embodiment, during performing the dry-forming andfunctionalizing step (as shown in the step 105 b), the resultedcomposite material is dried under a temperature of 90° C. to 150° C. for15 minutes to 30 minutes, for example, so as to remove the residualorganic solvent and to form the PCS-iron, as shown in the step 107. Inan example, the dry-forming and functionalizing step may be performed ina temperature of 100° C. to 120° C. In another example, the resultedPCS-iron may be formed in various shapes such as plates (or flakes orfilms), granules, hollow tubes or bars. For example, FIG. 2 shows anappearance of hollow tube-shaped ZVI-PCS according to an embodiment ofthe present invention. In a further example, the resulted ZVI-PCS mayhave a thickness of 1 μm to 1000 μm for example. In a still anotherexample, the resulted ZVI-PCS may have a thickness of 50 μm to 500 μm,for example.

The ZVI-PCS can be formed either alone as aforementioned or incombination with a substrate as follows. Optionally, before precedingthe forming and functionalizing step (as shown in the step 105), themixture can be uniformly coated onto the substrate by a suitably coatingmethod, in which various coating methods can be utilized in this coatingstep depending on different substrates. In an embodiment, the coatingmethod may be a blade coating or spin-on coating if the substrate is aplate (or a flake or a film). In another embodiment, the substrate maybe immersed into and coated with the mixture uniformly if the substrateis a granule, a hollow tube or a bar, thereby forming the mixtureuniformly on the surface of the substrate.

It is worth mentioning that, the aforementioned steps can be performedin a batch process or an automatically continuous process depending onthe requirements of the process. For example, reference is made to FIGS.3A to 3C, which show the photographs of cross-sectional (FIG. 3A),internal (FIG. 3B) and superficial (FIG. 3C) structures of the ZVI-PCSaccording to several embodiments of the present invention. Through theabove processes, the aforementioned ZVI-PCS produced by those steps iswell-functionalized, in which it has an internal coralloid-like channelstructure as shown in FIG. 3A), surface pores (as shown in FIG. 3B) withan averaged pore size of 1 nm to 100 μm.

In an embodiment, the ZVI-PCS, which is exemplified as a plate-likeZVI-PCS, a flake-like ZVI-PCS, a film-like ZVI-PCS, or a plate-likesubstrate coated with the ZVI-PCS, is immersed in a water-containingenvironment such as an ocean, a river, a lake, to sewerage, a ditch, anaquifer, a cistern, sludge or soil. In addition, the plate-like ZVI-PCS,the flake-like ZVI-PCS, the film-like ZVI-PCS, the bar-like ZVI-PCS orthose various shapes of the substrate coated with the ZVI-PCS can bemixed well with soil. And then, water molecules and pollutants diffuseinto the internal coralloid-like channel structure through the pores andthen contact with iron-containing materials and derivatives thereof inthe ZVI-PCS, so as to absorb and/or degrade the pollutants, continuouslyand stably release hydrogen in the outside the ZVI-PCS, therebyenhancing the growth of microbes in the water-containing environment.

In another embodiment, the ZVI-PCS, which may be formed either alone asaforementioned or in combination with the substrate coated with ZVI-PCScan be made into a barrier wall, for example, a permeable reactivebarrier (PRB), so as to in situ degrade contaminants which are passedthrough the PRB.

“The PRB” manufactured by the ZVI-PCS as described herein is referred toa PRB disposed along a cross-section of a flowing direction of a plumeof contaminants in the contaminated underground environment. The PRB canbe either a replaceable column established by using a well driller, orthe PRB established by digging ditches. The plume of contaminants can becaptured and/or broke down so as to be remove. Conventional powdercolumns or the PRBs are inconvenient for construction and replacementdue to them fixed beneath the ground. Furthermore, it costs more tobuild a conventional PRB that usually has a thickness of 2 meters to 3meters.

Specifically, reference is made to FIG. 4, which depicts a constructiondiagram of a replaceable column according to an embodiment of thepresent invention. In an example, multiple replaceable columns 403 areset up in an underground environment 400 that is contaminated bypollutants 402. The replaceable columns 403 can be established by usingdifferent construction methods along a diffusing direction 401 ofpollutants 402.

In an example, the replaceable columns 403 can be arranged in ahorizontal direction 411 corresponding to the pollutants' 402 diffusionand passed through an underlying environment of a pollutant source zoneA1.

In another example, the replaceable columns 403 can be also arranged byusing ropes in a vertical direction 413 corresponding to the pollutants'402 diffusion and passed through a channel 408 below a ditch 407 in anunderlying environment of a pollutant diffusion zone A2.

In a further example, the replaceable columns 403 can be furtherarranged by using ropes in a vertical direction 413 corresponding to thepollutants' 402 diffusion and passed through the channel 408 in anunderlying environment of a pollutant diffusion zone A2.

In a still further example, the replaceable columns 403 also can bearranged by using ropes in a vertical direction 413 corresponding to apollutant peripheral area A3 by using ropes along the vertical directionin the channel 408 to form fences. The replaceable columns 403 can bealso arranged by using ropes in a vertical direction 413 correspondingto the pollutants' 402 diffusion and passed through the channel 408 inan underlying environment of the pollutant peripheral area A3, therebyforming fences. Multiple rod-like ZVI-PCS 405 are further disposed inthe replaceable columns 403 to absorb and/or degrade pollutants 402 inthe contaminated underground environment 400 and release hydrogencontinually and stably, thereby promoting the growth of anaerobicmicrobes in the whole underlving environments contaminated by thepollutants 402.

Reference is made to FIG. 5, which depicts a diagram of a PRB accordingto another embodiment of the present invention. In the actual operation,the ZVI-PCS can be manufactured to a PRB 500. A wall 501 of the PRE 500can be made of commonly available materials, such as concrete or resin,and the width Wx and height Hy of the wall 501 can be freely adjusted,depending on the actual requirements. The thickness Dz of the wall 501is very thin, just 10 cm to 30 cm and preferably 10 cm to 15 cm, so thatconventionally available facilities such as tracks (unshown) or otherequivalent means can be utilized to take out the wall 501 easily forroutine replacement or maintenance. In addition, replaceable columns 503of the PRB 500 can be replaced freely and include multiple bar-likeZVI-PCS 500. Therefore, the PRB 500 of the present invention can improvethe shortcomings of the prior PRB such as inconvenient installation,difficult replacement and occupied spaces.

Thereinafter, various applications of the ZVI-PCS will be described inmore details referring to several exemplary embodiments below, while notintended to be limited. Thus, one skilled in the art can easilyascertain the essential characteristics of the present invention and,without departing from the spirit and scope thereof, can make variouschanges and modifications of the invention to adapt it to various usagesand conditions.

EXAMPLE 1 Preparation of ZVI-PCS

1. Preparation of Mixture

In this EXAMPLE, 1-methyl 2 pyrrolidione (NMP; 99+% purity,Spectrophotometer Grade, Merck Co., USA.) and polyethersulfone (PESF;Radel A-300, Ameco Performance, U.S.A.) as shown in following TABLE 1(Experimental Groups) were firstly added into a 500 mL glass bottle,slowly stirred until PESF was completely dissolved. The total volume ofNMP and PESF was 50 mL to 400 mL, for example, rather than being limitedthereto.

And then, ZVIs (averaged diameter of 20 nm to 10,000 nm approximately,GeoNano Environmental Technology, Inc., Taiwan) was added into thePESF/NMP solution, stirred in with a rotational speed of 500 rpm to 2000rpm for 2 hours and 24 hours, approximately, thereby evenly dispersingthe ZVIs in the PESF/NMP solution and forming a mixture.

TABLE 1 Amounts of Ingredients in the Mixture Absorbing material, heatPESF/NMP ZVI/PESF dispersing material Experimental (Weight (Weightand/or bionutrients Groups ratio) ratio) (ZVI + PESF) 1 1/5 92/8 0.01/100 to 35/100 2 1/5 60/40 3 1/5 50/50 4 1/5 25/75 5 1/5  5/95Control group — 100

Later, a dispersion and stabilization step was performed. In this step,a dispersant such as commercially available dispersants of Hypermer™KD-1, KD-2, KD-3, KD-4, KD-6, KD-7 and KD-9 manufactured by CrodaInternational Plc.England was added with an amount of 0.1 part to 2parts by weight based on the total weight of ZVIs and polymers (PESF)into the mixture, and stirred in with a rotational speed of 50 rpm to500 rpm for 6 hours and 24 hours approximately until the mixture wasmixed evenly and stably dispersed without immediate sedimentation. Thus,the iron-containing materials would be evenly dispersed in the ZVI-PCSduring a subsequent process, and the resulted PCS would have smoothsurface and uniform color.

2. Formation of ZVI-PCS

Following, a forming and functionalizing step was performed. The formingand functionalizing step included but was not limited to a wet-formingand functionalizing step and a dry-forming and functionalizing step, soas to make the mixture to form the ZVI-PCS. In this example, during thewet-forming and functionalizing step, the aforementioned mixture wasswollen in a coagulant in a temperature of 0° C. to 40° C. or 5° C. to15° C. for 0.5 minute to 5 minutes, for example, so as to remove the NMPand the coagulant mostly, thereby forming a composite material. Thecomposite material had a dense surface. The aforementioned coagulant wasmethanol, ethanol, propanol, acetone, water or any combination thereof.

During the dry-forming and functionalizing course, the swollen compositematerial was treated under a temperature of 90° C. to 150° C. or 100° C.to 120° C. for 15 minutes to 30 minutes, for example, for removing theresidual organic solvent and coagulant and forming a thickness of 1 μmto 1000 μm or 50 μm to 500 μm of ZVI-PCS on the substrate. The resultedZVI-PCS had an internal coralloid-like channel structure therein, asshown in FIG. 3B.

Optionally, the aforementioned mixture can be only performed thedry-forming and functionalizing step to form a thickness of 1 μm to 1000μm or 50 μm to 500 μm of ZVI-PCS film on the substrate. The resultedZVI-PCS film had a flexible and dense nonporous structure data notshown), and the ZVI-PCS film could further include the aforementionedheat dispersing materials.

In addition, before performing the forming and functionalizing step, theaforementioned mixture may be optionally coated onto the surface of thesubstrate uniformly by using conventionally blade coating or spin-oncoating methods. As exemplified by the blade coating method, dependingon what type of the blade coater was used, the mixture could be pouredinto a blade adjuster, and the coating thickness of the mixture may beadjusted by the height of the blade position. In an example, the heightof the blade position may be set at 100 μm to 200 μm or other heightrather than being limited thereto.

It is worth mentioning that, the aforementioned coating methods such asthe blade coating or spin-on coating methods are well known to theartisan in this art rather than being recited in detail herein.

When an automatically continuous process performs the aforementionedsteps, conveyor belts can transport the materials through a system toall the stages of the automatically continuous process, and the resultedZVI-PCS can be separated from the underlying conveyor belt.

EXAMPLE 2 Evaluation of Controlling Hydrogen Releasing Effect of ZVI-PCS

EXAMPLE 2 is related to evaluate the prolonged hydrogen-releasing effectof the ZVI-PCS of EXAMPLE 1 immersed in the water-containingenvironment.

Reference is made to FIG. 6, which depicts a schematic diagram of ameasurement device for measuring hydrogen accumulation released fromZVI-PCS of EXAMPLE 1 according to the present invention. In thisEXAMPLE, the measurement device 600 included a pair of a cartridge A anda cartridge B connected with each other in parallel through a tube 607.During measurement, a sample 601, such as ZVI powders or the ZVI-PCS ofEXAMPLE 1, could be put into the cartridge A, and then water 603 wasadded into the cartridge A and the cartridge B to the same level(height) of water. When the sample 601 was immersed in the water 603 fora period, hydrogen gas (H₂) could be continuously generated and thenpass through the tube 607 into a space 608 of the cartridge B. Theaccumulated hydrogen in the space 608 of the cartridge B pushed down onthe water surface and drained the overflow water 610 through the tube609 into a container 612, and the drained volume of the overflow water610 was equivalent to the volume of the accumulated hydrogen, so thatthe water level of the cartridge A was higher than the water level ofthe cartridge B up to a distance D. An opening (unshown) of the tube 409was connected to the container 612 and a little higher than the waterlevel in the cartridge B. Hence, the released hydrogen gas could bemeasured in milliliters (mL) by daily recording the drained volume ofthe overflow water 610.

Reference is made to FIG. 7, which depicts a curve diagram of releasedhydrogen amount of ZVI-PCS immersed in the device of FIG. 6. In FIG. 7,the horizontal axis is referred to the immersion duration (hour) of theZVI-PCS or bare ZVI powders, the vertical axis is referred to anaccumulated amount of released hydrogen per gram of ZVI (mL/g), which isthe volume of the overflowed water measured by the setup of FIG. 6 tothe theoretically generated hydrogen. In FIG. 7, the symbol ▴ isreferred to the released hydrogen accumulation of per gram of bare ZVI(mL/g), and the symbol ▪ is referred to the released hydrogenaccumulation of per gram of the ZVI-PCS(mL/g). The ZVI-PCS is granularand has a total weight of 1.13 g (containing 58 wt % of ZVIs).

According to the results in FIG. 7, the curves of the bare ZVIs (denotedas the symbol ▴) and the ZVI-PCS (denoted as the symbol ▪) had a littlesimilar trend of the released hydrogen accumulation. However, the bareZVIs (denoted as the symbol ▴) had a released hydrogen amount (mL/g)higher than the ZVI-PCS (denoted as the symbol ▪) because the bare ZVIsdirectly contacted water without the protection and control of the PCS(PESF) and the hydrogen gas was released very fast in a short period. Incomparison with the bare ZVIs, the ZVI-PCS of EXAMPLE 1 (denoted as thesymbol ▪ of FIG. 7) could have a slowly and stably released hydrogenaccumulation for more than 200 hours in the measurement device of FIG.6, so as to enhance the growth of anaerobic microbes in the sewerage.Meanwhile, the ZVI-PCS could absorb and/or degrade pollutants and notaffect the pH value of sewerage (data not shown).

Reference is made to FIG. 8, which depict a curve diagram ofoxidation-reduction potential (ORP; mV) of the ZVI-PCS. In FIG. 8, thehorizontal axis is referred to the immersed duration (hours) of theZVI-PCS or bare ZVIs, and the vertical axis is referred to the measuredORP of the solution where the ZVI-PCS is immersed in the device of FIG.6. In FIG. 8, the symbol ▪ is referred to the ORP (mV) of per gram ofthe bare ZVIs, and the symbol ♦ is referred to the oxidation reductionpotential (mV) of per gram of the ZVI-PCS. The ZVI-PCS is granular andhas a total weight of 1.13 g (containing 58 wt % of ZVIs).

According to the results in FIG. 8, the bare ZVIs (denoted as the symbol▪) directly contacted water without the protection and control of thePCS (PESF), so that the measured ORP declined rapidly to reduction stateand the hydrogen gas was released very fast in a short period of about0.15 hour. In comparison with the bare ZVIs, the ZVI-PCS of EXAMPLE 1released hydrogen slowly and stably in the measurement device of FIG. 6,so the ORP declined to reduction state until the hydrogen gas wasreleased for more than 0.8 hour, as shown as the symbol ♦ of FIG. 8), soas to enhance the growth of anaerobic microbes in the sewerage.

Reference is made to FIG. 9, which depict a curve diagram of molybdenum(Mo) concentration of Mo-containing wastewater treated by the ZVI-PCSaccording to an embodiment of the present invention. In FIG. 9, thehorizontal axis is referred to the amount (g/L) of the ZVI-PCS, and thevertical axis is referred to the Mo concentration (mg/L) of thewastewater. The test method can be referred to “Inductively coupledplasma-mass spectrum method (NIEA W313) for monitoring metals and traceelements in the water” announced by Environmental ProtectionAdministration Taiwan or other conventional test methods. The details ofmonitoring Mo concentration in water are well known by the artisan inthis art rather than being recited in detail herein.

According to the results in FIG. 9, the more ZVI-PCS was added into theMo-containing wastewater, the less Mo concentration would be existed inthe Mo--containing waste water. The result was evidenced that theZVI-PCS can effectively absorb the heavy metal Mo in the wastewater.

Reference is made to FIGS. 10A to 10C, which show a scanning electronmicroscopy image of the internal structure (FIG. 10A), an energydispersive spectrometry (EDS) image (FIG. 10B) and an element linescanning image (FIG. 10C) of the ZVI-PCS after treating theMo-containing wastewater according to an embodiment of the presentinvention, respectively, all of which is analyzed by high-resolutiontransmission electron microscopy (HR-TEM)—energy dispersive spectrometer(EDS) (Model No. JEM-2100F, JEOL Co.). The white arrows in FIGS. 10A and10C are referred to the scanning direction and distance from the surfaceto the core of the ZVI-PCS of an embodiment of the present invention.FIGS. 10B and 10C are the results of Mo distributed on the ZVI-PCSsurface.

According to the result of FIG. 10B, the element Mo was distributed onthe surface of the ZVI-PCS of an embodiment of the present invention.Moreover, the result of FIG. 10C revealed that the internalcoralloid-like channel structure in the ZVI-PCS can absorb the heavymetal Mo, thereby decreasing Mo concentration in the wastewater.

In other embodiments, when the permeable reactive barrier made of theZVI-PCS is disposed in the wastewater treatment equipment of asemiconductor fabrication plant for more than one month, pollutants inthe wastewater can be absorbed and/or degraded without changing pH valueof the overflowed wastewater in the sewage (data not shown).

In addition, in other embodiments, a nonporous film can be furthermanufactured by the ZVI-PCS for shielding electromagnetic waves (datanot shown).

In addition, it should be supplemented that, specific iron-containingmaterials and derivatives thereof, specific polymeric materials,specific polymeric carriers, specific reaction conditions, specificsubstrates, specific apparatuses or specific water-containingenvironments are exemplified in the present invention for clarifying theZVM-PCS of the present invention; however, as is understood by a personskilled in the art, other iron-containing materials and derivativesthereof, other polymeric carriers, other reaction conditions, othersubstrates, other apparatuses or other water-containing environments canbe also used in the production of the ZVM-PCS of the present invention,rather than limiting thereto.

According to the embodiments of the present invention, theaforementioned ZVM-PCS and manufacturing method thereof, theyadvantageously include that the internal coralloid-like channelstructure of PCS can be tunable to accommodate high amount of theiron-containing materials and derivatives thereof and control thehydrogen-releasing rate. The surface pore size, porosity,hydrophilicity, and internal coralloid-like channel structure of PCS canbe tailored through the manufacturing process, so that PCS can befunctioned as a regulator for the releasing of produced hydrogen, andalso control the adsorption and reduction reactions toward heavy metalsand chlorinated volatile organic compounds in water. The releasedhydrogen from the ZVM-PCS can enhance the growth and metabolism ofanaerobic organisms in the water-containing environment. Moreover, theZVM-PCS can be developed as the filter materials that can be installedin a column or any storage for water and wastewater treatment, or evenin a groundwater cut-off barrier for the cleanup of contamination. Whilethe ZVM-PCS is synthesized as a film without surface openings, it can beused as the EMI shielding material.

As is understood by a person skilled in the art, the foregoingembodiments of the present invention are illustrated of the presentinvention rather than limiting of the present invention. It is intendedto cover various modifications and similar arrangements included withinthe spirit and scope of the appended claims. Therefore, the scope ofwhich should be accorded the broadest interpretation so as to encompassall such modifications and similar structure.

1. A zerovalent metal-polymer complex supporter (ZVM-PCS), comprising: 1part to 92 parts by weight of iron-containing materials and derivativesthereof, wherein the iron-containing materials and derivatives thereofcomprises zero-valent irons and has an averaged diameter from 1nanometer (nm) to 10 micrometers μm); and 8 parts to 99 parts by weightof polymer complex supporter (PCS), wherein the PCS and theiron-containing materials and derivatives thereof are mixed well, thePCS possesses an internal coralloid-like channel structure and surfacepores with an averaged pore size from 1 nm to 100 μm, and wherein as theZVM-PCS is delivered into a water-containing environment, watermolecules and pollutants can diffuse into the internal coralloid-likechannel structure through the surface pores and then react with theiron-containing materials and derivatives thereof, so as to adsorband/or degrade the pollutants and continuously release out hydrogenthrough the surface pores, thereby enhancing anaerobic bioremediationprocess in the water-containing environment.
 2. The ZVM-PCS according toclaim 1, wherein the iron-containing materials and derivatives thereoffurther comprises precious metals to coat on the zero-valent irons, andthe precious metals are selected from the group consisting of platinum,palladium, rhodium, gold, silver, cobalt and any combination thereof. 3.The ZVM-PCS according to claim 1, wherein the amount of theiron-containing materials and derivatives thereof in PCS is from 10parts to 92 parts by weight.
 4. The ZVM-PCS according to claim 1,wherein the pollutants is heavy metal pollutants, organohalogencompounds or nitrates, and the heavy metal pollutants comprises arsenicor chromium, and the organohalogen compounds comprises chlorinatedvolatile organic compounds (CVOCs), trichloroethylene (TCE),perchloroethylene (PCE) or dioxins.
 5. The ZVM-PCS according to claim 1,wherein polymers belong to sulfone polymers or fluorine-containingpolymers, and the amount of the polymers is 8 parts to 50 parts byweight.
 6. The ZVM-PCS according to claim 5, wherein the sulfonepolymers are selected from the group consisting of polyethersulfone(PESF), polysulfone (PSF) and polyphenylene sulfone (PPSF).
 7. TheZVM-PCS according to claim 6, wherein the fluorine-containing polymer ispolyvinylidene fluoride (PVDF).
 8. The ZVM-PCS according to claim 1,further comprising absorbent materials, wherein the amount of theabsorbent materials in the ZVM-PCS is 0.01 part to 35 parts by weight,and the absorbent materials are selected from the group consisting ofactivated carbon, zeolite, molecular sieve and any combination thereof.9. The ZVM-PCS according to claim 1, further comprising heat dispersingmaterials, wherein the amount of the heat dispersing materials in theZVM-PCS is 0.01. part to 35 parts by weight, and the heat dispersingmaterials are selected from the group consisting of boron nitride,carbon nanotubes and any combination thereof.
 10. The ZVM-PCS accordingto claim 1, further comprising bionutrients, wherein the amount of thebionutrients in the ZVM-PCS is 0.01 part to 35 parts by weight, and thebionutrients are selected from the group consisting of sugar, starch andany combination thereof.
 11. The ZVM-PCS according to claim 1, furthercomprising dispersants, wherein the amount of the dispersants in theZVM-PCS is 0.1 part to 2 parts by weight, and the dispersants areselected from the group consisting of polycarbonate, polyvinyl alcohol,polyacrylamide and any combination thereof.
 12. The ZVM-PCS according toclaim 1, wherein the water-containing environment refers to ocean,river, lake, sewerage, ditch, aquifer, cistern, sludge or soil.
 13. Amethod for manufacturing ZVM-PCS, comprising: preparing a mixture,wherein the mixture comprises: 1 part to 99 parts by weight ofiron-containing materials and derivatives thereof, wherein theiron-containing materials and derivatives thereof comprise zero-valentirons and have an averaged diameter from 1 nm to 10 μm; and 8 parts to99 parts by weight of polymers, wherein the polymers belong to sulfonepolymers or fluorine-containing polymers; and an organic solvent todissolve the polymers and to disperse the iron-containing materials andderivatives thereof uniformly wherein the organic solvent is selectedfrom the group consisting of N,N-dimethyl formamide (DMF), 1-methyl 2pyrrolidione (NMP) and N,N-dimethylacetamide (DMAc); conducting avacuuming step to remove air bubbles in the mixture; and conducting aforming and functionalizing step, wherein the forming andfunctionalizing step comprises: performing a wet-forming andfunctionalizing step, the as-synthesized material is performed in acoagulating solvent in a temperature range from 0° C. to 40° C. for 0.5minute to 5 minutes, which removes part of the organic solvent and formsa complex. The coagulating solvents are selected from the groupconsisting of methanol, ethanol, propanol, acetone, water and anycombination thereof; and performing a dry-forming and functionalizingstep, to keep the composite material to be dried in a temperature of 90°C. to 150° C. for 15 minutes to 30 minutes, so as to remove a residue ofthe organic solvent and the coagulant and to form the ZVM-PCS thataccommodates the iron-containing materials and derivatives thereof, andthe ZVM-PCS has a thickness of 1 μm to 1000 μm.
 14. The method formanufacturing ZVM-PCS according to claim 13, wherein an amount of theiron-containing materials and derivatives thereof in the ZVM-PCS is 50parts to 92 parts by weight.
 15. The method for manufacturing ZVM-PCSaccording to claim 13, wherein the iron-containing materials andderivatives thereof further comprises precious metals to coat on thezero-valent irons, and the precious metals are selected from the groupconsisting of platinum, palladium, rhodium, gold, silver, cobalt and ancombination thereof.
 16. The method for manufacturing ZVM-PCS accordingto claim 13, wherein the sulfone polymer is selected from the groupconsisting of PESF, PSF and PPSF, and an amount of the sulfone polymerin the ZVM-PCS is 8 parts to 50 parts by weight.
 17. The method formanufacturing ZVM-PCS according to claim 13, wherein thefluorine-containing polymer is PVDF, and an amount of thefluorine-containing polymer in the ZVM-PCS is 8 parts to 50 parts byweight.
 18. The method for manufacturing ZVM-PCS according to claim 13,wherein the mixture further comprises an absorbent material, an amountof the absorbent materials in the ZVM-PCS is 0.01 part to 35 parts byweight, and the absorbent material is selected from the group consistingof activated carbon, zeolite, molecular sieve and any combinationthereof.
 19. The method for manufacturing ZVM-PCS according, to claim13, wherein the mixture further comprises a heat dispersing material, anamount of the heat dispersing material in the ZVM-PCS is 0.01 part to 35parts by weight, and the heat dispersing material is selected from thegroup consisting of boron nitride, carbon nanotubes and any combinationthereof.
 20. The method for manufacturing ZVM-PCS according to claim 13,wherein the mixture further comprises a bionutrient, an amount of thebionutrients in the ZVM-PCS is 0.01 part to 35 parts by weight, and thebionutrients is selected from the group consisting of sugar, starch,phosphate and any combination thereof.
 21. The method for manufacturingZVM-PCS according to claim 13, wherein the mixture further comprises adispersant, an amount of the dispersant in the ZVM-PCS is 0.1 part to 2parts by weight, and the dispersant is selected from the groupconsisting of polycarbonate, polyvinyl alcohol, polyacrylamide and anycombination thereof.
 22. The method for manufacturing ZVM-PCS accordingto claim 13, wherein the ZVM-PCS has a flake-like, granule-like, ahollow tube-like or a rod-like shape.
 23. The method for manufacturingZVM-PCS according to claim 13, further comprising: conducting a coatingstep to keep the mixture being formed on a substrate, wherein thecoating step is a spin-on coating step or a blade coating step.
 24. Themethod for manufacturing ZVM-PCS according to claim 23, wherein theZVM-PCS is shaped as a thin film, a granule, a hollow tube or a rod. 25.The method for manufacturing ZVM-PCS according to claim 13, wherein thevacuuming step is performed for 10 minutes to 30 minutes.
 26. The methodfor manufacturing ZVM-PCS according to claim 13, wherein the method formanufacturing the ZVM-PCS is performed in a batch process or anautomatically continuous process.
 27. The method for manufacturingZVM-PCS according to claim 13, wherein the PCS possesses an internalcoralloid-like channel structure and a porous surface with an averagedpore size from 1 nm to 100 μm, and as the ZVM-PCS is immersed in awater-containing environment, water molecules and pollutants can diffuseinto the internal coralloid-like channel structure through the surfacepores and then contact with the iron-containing materials andderivatives thereof, so as to adsorb and/or degrade the pollutants andcontinuously release out hydrogen through the surface pores, therebyenhancing anaerobic bioremediation process in the water-containingenvironment.
 28. The method for manufacturing ZVM-PCS according to claim27, wherein the water-containing environment refers to ocean, river,lake, sewerage, ditch, aquifer, cistern, sludge or soil.
 29. The methodfor manufacturing LVM-PCS according to claim 27, wherein the pollutantsis heavy metal pollutants, organohalogen compounds or nitrates, and theheavy metal pollutants comprises arsenic or chromium, and theorganohalogen compounds comprises chlorinated volatile organic compounds(CVOCs), trichloroethylene (TCE), perchloroethylene (PCE) or dioxins.30. A method for manufacturing ZVM-PCS, comprising: preparing a mixture,wherein the mixture comprises: 1 part to 99 parts by weight ofiron-containing materials and derivatives thereof, wherein theiron-containing materials and derivatives thereof comprise zero-valentirons and have an averaged diameter from 1 nm to 10 μm; and 8 parts to99 parts by weight of polymers, wherein the polymers belong to sulfonepolymers or fluorine-containing polymers; and an organic solvent todissolve the polymers and to disperse the iron-containing materials andderivatives thereof uniformly wherein the organic solvent is selectedfrom the group consisting of N,N-dimethyl formamide (DMF), 1-methyl 2pyrrolidione (NMP) and N,N-dimethylacetamide (DMAc); conducting avacuuming step to remove air bubbles in the mixture; and performing adry-forming and functionalizing step, to keep the composite material tobe dried in a temperature of 90° C. to 150° C. for 15 minutes to 30minutes, so as to remove a residue of the organic solvent and thecoagulant and to form the ZVM-PCS that accommodates the iron-containingmaterials and derivatives thereof, and the ZVM-PCS is flexible and has adense non-porous structure with thickness from 1 μm to 1000 μm.
 31. Themethod for manufacturing ZVM-PCS according to claim 30, wherein anamount of the iron-containing materials and derivatives thereof in theZVM-PCS is 50 parts to 92 parts by weight.
 32. The method formanufacturing ZVM-PCS according to claim 30, wherein the iron-containingmaterials and derivatives thereof further comprises precious metals tocoat on the zero-valent irons, and the precious metals are selected fromthe group consisting of platinum, palladium, rhodium, gold, silver,cobalt and any combination thereof.
 33. The method for manufacturingZVM-PCS according to claim 30, wherein the sulfone polymer is selectedfrom the group consisting of PESF, PSF and PPSF, and an amount of thesulfone polymer in the ZVM-PCS is 8 parts to 50 parts by weight.
 34. Themethod for manufacturing ZVM-PCS according to claim 30, wherein thefluorine-containing polymer is PVDF, and an amount of thefluorine-containing polymer in the ZVM-PCS is 8 parts to 50 parts byweight.
 35. The method for manufacturing ZVM-PCS according to claim 30,wherein the mixture further comprises a heat dispersing material, anamount of the heat dispersing material in the ZVM-PCS is 0.01 part to 35parts by weight, and the heat dispersing material is selected from thegroup consisting of boron nitride, carbon nanotubes and any combinationthereof.
 36. The method for manufacturing ZVM-PCS according to claim 30,wherein the mixture further comprises a dispersant, an amount of thedispersant in the ZVM-PCS is 0.1 part to 2 parts by weight, and thedispersant is selected from the group consisting of polycarbonate,polyvinyl alcohol, polyacrylamide and any combination thereof.
 37. Themethod for manufacturing ZVM-PCS according to claim. 30, wherein theZVM-PCS has a flake-like shape.
 38. The method for manufacturing ZVM-PCSaccording to claim 30, further comprising: conducting a coating step tokeep the mixture being formed on a substrate, wherein the coating stepis a spin-on coating step or a blade coating step.
 39. The method formanufacturing ZVM-PCS according to claim 38, wherein the ZVM-PCS isshaped as a thin film, a granule, a hollow tube or a rod.
 40. The methodfor manufacturing ZVM-PCS according to claim 30, wherein the vacuumingstep is performed for 10 minutes to 30 minutes.
 41. The method formanufacturing ZVM-PCS according to claim 30, wherein the method formanufacturing ZVM-PCS is performed in a batch process or anautomatically continuous process.
 42. An electromagnetic interference(EMI) shielding material obtained by the method of claims 30.